A concentrated solar still is a system that uses the same amount of solar heat input (same solar collection area) as a simple solar still but can produce a volume of water that is many times greater. While a single solar still is a way of distilling water by using the heat of the sun to drive evaporation from a water source and ambient air to cool a condenser film, Concentrated solar still uses a Concentrated solar thermal collector to concentrate solar heat and deliver it to a multi-effect evaporationprocess for distillation, thus increasing the natural rate of evaporation. The concentrated solar still is capable of large-scale water production in areas with solar energy.
The concentrated solar still can produce more than 20x more water than the theoretical maximum of a standard solar still   and in practice, can produce as much as 30x volume. For instance, with a solar collection area of 10 acres, a standard solar still operating at a typical 25% efficiency  may produce as much as 27.8acre-ft / yr in a region with an average daily solar irradiation value of 21.6MJ / m². A concentrated solar still can produce more than 750acre-ft / yr in the same region with the same collection area.
Multiple stage evaporation
The concentrated solar still implements a method for recovering the latent heat of the distillate vapor not captured and reused by a standard solar still. This is done by using multiple stages of evaporation in series (see multiple-effect evaporator ). The latent heat of the distillate vapor produced in the n-1 stage (or effect) is recovered in the nth stage by boiling the leftover concentrated brine from the n-1 stage which produces distillate vapor which will be recovered in the n + 1 1 stage by boiling the leftover concentrated brine from the nth stage. Since brine is in the process of being standardized, it will be subject to standard conditions. To overcome the boiling point elevation of the brine, each evaporator stage operates at a lower pressure than the previous stage, which effectively reduces the boiling point, allowing for sufficient heat transfer to take place in each stage. This process can be repeated until the distillate conditions are sufficiently degraded (ie, very low pressure and very low volume). 
The final evaporation stage is distillate vapor that is considered to be at very poor state conditions. This vapor can be condensed in a final condenser, in which case its latent heat is as waste,  or it can be condensed by using a heat pump, in which case its latent heat (or a portion of it) can be recovered. In the latter case, the heat pump effectively “upgrades” the state conditions of the latent heat to more usable conditions (higher temperature and pressure) by performing work (eg, compression).   The conditions can be upgraded in such a way that they can be used to provide additional heat for evaporation in the first effect.
- ^ Jump up to:a b Alarcon-Padilla, Diego C .; Garcia-Rodriguez, Lourdes; Blanco-Galvez, Julian (2010). “Design Recommendations for a Multi-Effect Plant Distillation Connected to a Double-Absorption Heat Pump Effect: A Solar Desalination Case Study”. Desalination . 262 : 11-14. doi : 10.1016 / j.desal.2010.04.064 .
- ^ Jump up to:a b Alarcon-Padilla, Diego C .; Garcia-Rodriguez, Lourdes; Blanco-Galvez, Julian (2010). “Experimental Assessment of Heat Pump Absorption to a Multi-Effect Distillation Unit” . Desalination . 250 : 500-505. doi : 10.1016 / j.desal.2009.06.056 .
- Jump up^ “Solar Distillation: Technical Brief” (PDF) . engineeringforchange.org . Retrieved 25 August 2013 .
- ^ Jump up to:a b Geankoplis, John Christie (2004). Transport Processes and Separation Process Principles . Upper Saddle Creek: Prentice Hall .
- Jump up^ “Solar Desalination – Clean Water from Solar Energy” (PDF) . Aalborg CSP . Retrieved 31 March 2017 .